A furnace burns a liquid coal tar fuel derived from coke-ovens. Calculate the heat transferred in the furnace if the combustion gases leave at 1500 K. The burners operate with 20 per cent excess air. Take the fuel supply temperature as 50ºC (323 K) and the air temperature as 15ºC (288 K).
The properties of the fuel are:
Carbon 87.5 per cent w/w
Hydrogen 8.0
Oxygen 3.5
Nitrogen 1.0
Sulphur trace
Ash balance
Net calorific value 39,540 kJ/kg
Latent heat of vaporisation 350 kJ/kg
Heat capacity 1.6 kJ/kg K
\ C^{º}_{p} of gases, kJ/kmol K
\ C_{p} =A+BT+CT^{2} +DT^{3}
D | C | B | A | Camponent |
17.125E-9 | -5.518E-5 | 7.332E-2 | 19.763 | 1 \ CO_{2} |
-3.591E-9 | 10.538E-6 | 19.207E-4 | 32.190 | 2 \ H_{2}O |
-10.634E-9 | 17.431E-6 | -3.674E-6 | 28.06 | 3 \ O_{2} |
-11.662E-9 | 26.752E-2 | -1.354E-2 | 31.099 | 4 \ N_{2} |